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    • 2. 发明授权
    • Polymeric porous hollow fiber membrane
    • 聚合多孔中空纤维膜
    • US08881915B2
    • 2014-11-11
    • US12298456
    • 2007-04-25
    • Hideyuki YokotaNoriaki KatoHirofumi OgawaJunsuke Morita
    • Hideyuki YokotaNoriaki KatoHirofumi OgawaJunsuke Morita
    • B01D39/16B01D63/02B01D63/06B01D69/08D01F1/08B32B3/12B01D71/68B01D71/44B01D69/02
    • B01D69/087B01D69/02B01D69/08B01D71/44B01D71/68B01D2325/022B01D2325/36B01D2325/38Y10T428/249921Y10T428/249978Y10T428/249979Y10T428/24998Y10T428/2975
    • PURPOSE: To provide a polymeric porous hollow fiber membrane which exhibits excellent fractionation performance and excellent permeability in treatment of a variety of aqueous fluids and also shows sufficient strength when incorporated into a module or used to treat a fluid, and which is excellent in aging stability in these performances and characteristics and is also excellent in membrane performance recoverability by washing, and which is especially suitable for treatment of a polyphenol-containing beverage and is expected to effectively harmonize the flavor of such a beverage.SOLUTION: A polymeric porous hollow fiber membrane of the present invention is characterized in that (a) the hollow fiber membrane has skin layers on its inner and outer surfaces; (b) the diameters of the pores in the inner surface are smaller than the diameters of the pores in the outer surface; (c) the porosity tends to increase from the inner surface toward the outer surface, and then tends to decrease from at least one portion having a maximum porosity, of the wall section of the membrane, toward the outer surface; and (d) the hollow fiber membrane satisfies a relationship of 2 [%]≦DR≦20 [%], wherein the critical diameter of a fine particle to be removed, found by a fine particle-passing test, is φmax [μm]; the diameter of the pores in the inner surface is dIS [μm]; and the proportion of the pores with dIS exceeding φmax is DR [%]. This polymeric porous hollow fiber membrane is also characterized in that the adsorption of polyphenol per a surface area of 1 m2 defined by the inner and outer surfaces of the membrane is from 50 to 500 mg.
    • 目的:提供一种聚合多孔中空纤维膜,其在各种水性流体的处理中表现出优异的分级性能和优异的渗透性,并且当结合到模块中或用于处理流体时也显示出足够的强度,并且其老化稳定性优异 在这些性能和特性中,通过洗涤也具有优异的膜性能可回收性,并且其特别适用于处理含多酚饮料,并且预期能有效地协调这种饮料的风味。 解决方案:本发明的聚合物多孔中空纤维膜的特征在于:(a)中空纤维膜在其内表面和外表面上具有表皮层; (b)内表面的孔的直径小于外表面的孔的直径; (c)孔隙率从内表面朝向外表面增加,然后趋向于从膜的壁部的最大孔隙率的至少一部分朝向外表面减小; 和(d)中空纤维膜满足2 [%]≦̸ DR≦̸ 20 [%]的关系,其中通过细粒通过试验发现的要除去的微粒的临界直径为最大 [μm]; 内表面孔的直径为dIS [μm]。 dIS超过最大孔的比例为DR [%]。 该聚合物多孔中空纤维膜的特征还在于,由膜的内表面和外表面限定的1m 2表面积的多酚的吸附量为50〜500mg。
    • 3. 发明申请
    • POROUS HOLLOW FIBER MEMBRANE AND A POROUS HOLLOW FIBER MEMBRANE FOR THE TREATMENT OF A PROTEIN-CONTAINING LIQUID
    • 多孔中空纤维膜和多孔中空纤维膜用于处理含蛋白质的液体
    • US20110259816A1
    • 2011-10-27
    • US13142125
    • 2009-12-24
    • Hideyuki YokotaNoriaki KatoHirofumi OgawaJunsuke Morita
    • Hideyuki YokotaNoriaki KatoHirofumi OgawaJunsuke Morita
    • B01D69/08
    • B01D71/68B01D69/02B01D69/08B01D69/081B01D69/087B01D2239/1233B01D2239/1258B01D2325/02B01D2325/021B01D2325/022B01D2325/023B01D2325/20
    • The purpose of the present invention is to provide a porous hollow fiber membrane that can efficiently separate and remove the substances to be removed such as small-particle virus contained in a solution and, at the same time, useful recovering substances such as protein can be efficiently permeated and the decrease of its transmission rate with elapse of time is small. The porous hollow fiber membrane of the present invention is characterized in that the filtration downstream surface thereof has dot-shaped or slit-shaped pores, the filtration upstream surface thereof is a network structure or a fine particle aggregate structure, the central region of the membrane is composed of a substantially homogeneous structure, the membrane wall is composed of a structure having substantially no macrovoids, the permeability for pure water is 10 to 300 L/(h·m2·bar) and the permeability for a 0.1% by weight solution of bovine γ-globulin is 30 to 100% of the permeability for pure water. Also, the hollow fiber membrane is characterized in that the permeability for a 0.1% by weight solution of bovine γ-globulin in a 20 mmol/L phosphate buffer is 30 to 100% of the permeability for a 0.1% by weight solution of bovine γ-globulin in a 20 mmol/L phosphate-buffered physiological saline solution.
    • 本发明的目的是提供一种多孔中空纤维膜,其能够有效地分离除去溶解物中所含的小粒子病毒等被除去物质,并且同时可用于回收物质如蛋白质可以是 有效渗透,随着时间的流逝,传播速率的下降也很小。 本发明的多孔中空纤维膜的特征在于,其过滤下游表面具有点状或狭缝状的孔,其过滤上游面为网状结构或细颗粒聚集体结构,膜的中心区域 由基本上均匀的结构构成,膜壁由基本上没有大孔的结构构成,纯水的渗透性为10〜300L /(h·m 2·bar),并且0.1重量%的 牛γ-球蛋白是纯水的渗透性的30〜100%。 此外,中空纤维膜的特征在于,0.1%重量的牛γ-球蛋白溶液在20mmol / L磷酸盐缓冲液中的渗透性为0.1%(重量)牛γ溶液的渗透性的30〜100% - 球蛋白在20 mmol / L磷酸盐缓冲生理盐水溶液中。
    • 4. 发明授权
    • Hollow fiber membrane for treating liquids
    • 用于处理液体的中空纤维膜
    • US08225941B2
    • 2012-07-24
    • US12682814
    • 2008-10-16
    • Hirofumi OgawaNoriaki KatoHideyuki YokotaJunsuke Morita
    • Hirofumi OgawaNoriaki KatoHideyuki YokotaJunsuke Morita
    • B01D33/21B01D39/00B01D39/14B01D70/28
    • C02F1/444B01D69/02B01D69/081B01D2325/022B01D2325/04
    • The present invention provides a hollow fiber membrane for treating liquids. When used for a hollow fiber membrane module for refining a fermented liquid such as beer or wine, the hollow fiber membrane exhibits a high filtration performance per unit area thereof, with reduced clogging of the membrane. The membrane performance is sufficiently recovered by washing.The present invention is a hollow fiber membrane for treating liquids, wherein a ratio of Flux 120 to Flux 30 is 0.45 or higher when filtration is performed by supplying a solution having a turbidity of 20 NTU into a hollow fiber membrane having an internal diameter of 500 to 1500 μm and a membrane thickness of 100 to 500 μm with a transmembrane pressure of 1.5 bar, the Flux 30 being flux 30 minutes after the start of the filtration, the Flux 120 being flux 120 minutes after the start of the filtration.
    • 本发明提供一种用于处理液体的中空纤维膜。 当用于中空纤维膜组件用于精炼啤酒或葡萄酒等发酵液时,中空纤维膜的单位面积显示出高的过滤性能,同时膜的堵塞减少。 通过洗涤充分回收膜性能。 本发明是用于处理液体的中空纤维膜,其中当通过将具有20NTU的浊度的溶液供应到内径为500的中空纤维膜中时,通量120与通量30的比例为0.45或更高 至1500微米,膜厚为100至500微米,跨膜压力为1.5巴,Flux 30在开始过滤后30分钟通入,Flux 120在开始过滤120分钟后通入。
    • 5. 发明申请
    • HOLLOW FIBER MEMBRANE FOR TREATING LIQUIDS
    • 中空纤维膜用于处理液体
    • US20100219122A1
    • 2010-09-02
    • US12682814
    • 2008-10-16
    • Hirofumi OgawaNoriaki KatoHideyuki YokotaJunsuke Morita
    • Hirofumi OgawaNoriaki KatoHideyuki YokotaJunsuke Morita
    • B01D69/08
    • C02F1/444B01D69/02B01D69/081B01D2325/022B01D2325/04
    • The present invention provides a hollow fiber membrane for treating liquids. When used for a hollow fiber membrane module for refining a fermented liquid such as beer or wine, the hollow fiber membrane exhibits a high filtration performance per unit area thereof, with reduced clogging of the membrane. The membrane performance is sufficiently recovered by washing.The present invention is a hollow fiber membrane for treating liquids, wherein a ratio of Flux 120 to Flux 30 is 0.45 or higher when filtration is performed by supplying a solution having a turbidity of 20 NTU into a hollow fiber membrane having an internal diameter of 500 to 1500 μm and a membrane thickness of 100 to 500 μm with a transmembrane pressure of 1.5 bar, the Flux 30 being flux 30 minutes after the start of the filtration, the Flux 120 being flux 120 minutes after the start of the filtration.
    • 本发明提供一种用于处理液体的中空纤维膜。 当用于中空纤维膜组件用于精炼啤酒或葡萄酒等发酵液时,中空纤维膜的单位面积显示出高的过滤性能,同时膜的堵塞减少。 通过洗涤充分回收膜性能。 本发明是用于处理液体的中空纤维膜,其中当通过将具有20NTU的浊度的溶液供应到内径为500的中空纤维膜中时,通量120与通量30的比例为0.45或更高 至1500微米,膜厚为100至500微米,跨膜压力为1.5巴,Flux 30在开始过滤后30分钟通入,Flux 120在开始过滤120分钟后通入。
    • 6. 发明申请
    • POLYMERIC POROUS HOLLOW FIBER MEMBRANE
    • 聚合多孔中空纤维膜
    • US20090110900A1
    • 2009-04-30
    • US12298456
    • 2007-04-25
    • Hideyuki YokotaNoriaki KatoHirofumi OgawaJunsuke Morita
    • Hideyuki YokotaNoriaki KatoHirofumi OgawaJunsuke Morita
    • B32B3/26B32B5/24
    • B01D69/087B01D69/02B01D69/08B01D71/44B01D71/68B01D2325/022B01D2325/36B01D2325/38Y10T428/249921Y10T428/249978Y10T428/249979Y10T428/24998Y10T428/2975
    • Purpose: To provide a polymeric porous hollow fiber membrane which exhibits excellent fractionation performance and excellent permeability in treatment of a variety of aqueous fluids and also shows sufficient strength when incorporated into a module or used to treat a fluid, and which is excellent in aging stability in these performances and characteristics and is also excellent in membrane performance recoverability by washing, and which is especially suitable for treatment of a polyphenol-containing beverage and is expected to effectively harmonize the flavor of such a beverage. Solution: A polymeric porous hollow fiber membrane of the present invention is characterized in that (a) the hollow fiber membrane has skin layers on its inner and outer surfaces; (b) the diameters of the pores in the inner surface are smaller than the diameters of the pores in the outer surface; (c) the porosity tends to increase from the inner surface toward the outer surface, and then tends to decrease from at least one portion having a maximum porosity, of the wall section of the membrane, toward the outer surface; and (d) the hollow fiber membrane satisfies a relationship of 2 [%]≦DR≦20 [%], wherein the critical diameter of a fine particle to be removed, found by a fine particle-passing test, is φmax [μm]; the diameter of the pores in the inner surface is dIS [μm]; and the proportion of the pores with dIS exceeding φmax is DR [%] This polymeric porous hollow fiber membrane is also characterized in that the adsorption of polyphenol per a surface area of 1 m2 defined by the inner and outer surfaces of the membrane is from 50 to 500 mg.
    • 目的:提供一种聚合多孔中空纤维膜,其在各种水性流体的处理中表现出优异的分级性能和优异的渗透性,并且当结合到模块中或用于处理流体时也显示出足够的强度,并且其老化稳定性优异 在这些性能和特性中,通过洗涤也具有优异的膜性能可回收性,并且其特别适用于处理含多酚饮料,并且预期能有效地协调这种饮料的风味。 解决方案:本发明的聚合物多孔中空纤维膜的特征在于,(a)中空纤维膜在其内表面和外表面上具有表皮层; (b)内表面的孔的直径小于外表面的孔的直径; (c)孔隙率从内表面朝向外表面增加,然后趋向于从膜的壁部的最大孔隙率的至少一部分朝向外表面减小; 和(d)中空纤维膜满足2 [%] <= DR <= 20 [%]的关系,其中通过微粒通过试验发现的要除去的微粒的临界直径为p​​himax [ 妈妈] 内表面的孔的直径为dIS [mum]; 并且dIS超过phimax的孔的比例为DR [%]。该聚合物多孔中空纤维膜的特征还在于,由膜的内表面和外表面限定的表面积为1m 2的多酚的吸附量为50 至500mg。
    • 7. 发明申请
    • BLOOD PURIFIER
    • 血液净化器
    • US20090272686A1
    • 2009-11-05
    • US11910627
    • 2006-04-03
    • Kimihiro MabuchiHideyuki YokotaKatsuaki KuzeNoriko MondenNoriaki KatoMakoto OhnoMitsuru Suzuki
    • Kimihiro MabuchiHideyuki YokotaKatsuaki KuzeNoriko MondenNoriaki KatoMakoto OhnoMitsuru Suzuki
    • B01D69/08
    • B01D69/02A61M1/16A61M2209/06B01D67/0011B01D67/009B01D69/08B01D71/44B01D71/68B01D2325/20B01D2325/28C02F1/44C02F2103/026
    • [Purpose] To provide a blood purifier which has high levels of blood compatibility, performance-retaining property when in contact with blood, and safety, and which shows an excellent water permeability-exhibiting rate after a priming treatment and has high reliability in long-term storage.[Solution] A blood purifier assembled using a polyvinyl pyrrolidone-containing polysulfone-based permselective hollow fiber membrane bundle, characterized in that the amount of polyvinyl pyrrolidone which elutes from the hollow fiber membrane bundle is 10 ppm or less, the amounts of hydrogen peroxide which elute from extracts from all the sites of the hollow fiber membrane bundle are 5 ppm or less, when the hollow fiber membrane bundle is divided into 10 portions in the lengthwise direction to test the sites of all the 10 portions according to the method regulated in the Approval Standard for Dialysis-Type Artificial Kidney Apparatus, and the water permeability of the blood purifier found at a point of time when 10 minutes has passed since the priming treatment of the blood purifier is 90% or more of the water permeability of the same found at a point of time when 24 hours has passed since the priming treatment thereof.
    • [目的]提供一种具有高血液相容性,与血液接触时的性能保持性和安全性的血液净化器,并且在预处理后显示出优异的透水性,并且在长期使用中具有高可靠性, 长期存储。 [解决方案]使用含聚乙烯吡咯烷酮的聚砜系渗透性中空纤维膜束组装的血液净化器,其特征在于,从中空纤维膜束洗出的聚乙烯吡咯烷酮的量为10ppm以下,过氧化氢的量 从中空纤维膜束的所有位置的提取物中洗脱出的浓度为5ppm以下,将中空纤维膜束沿长度方向分割成10份,按照本发明的方法 透析型人造肾器的认可标准和自血液净化器起动处理10分钟后发现的血液净化器的透水性为同一发现的透水性的90%以上 在自启动处理24小时后的时间点。